Rubber-like, elastic thermoplastic polyurethane having a hardness Shore A lower than 80

Abstract: A thermoplastic polyurethane having a hardness Shore A lower than 80, is prepared by reacting a) an aromatic diisocynate selected among 4,4'-diphenylmethane-diisocynate (MDI), 2,4-tolylene-diisocyanate (TDI) and 1,5-napthylene-diisocyanate (NDI), b) a polyhydroxy compound selected among the adipic acid/butanediol, adipic acid/monoethylene glycol (MEG) and adipic acid/hexanediol polyesters, polycaprolactones and polyethers obtained by polymerization of hydroxylated tetrahydrofuran compounds, and c) a chain extender selected between monoethylene glycol and bismetahydroxyethoxybenzene.

Description: This invention relates to an elastic and rubber-like thermoplastic polyurethane having a hardness Shore A lower than 80 and a remarkable elastic flow, a process for the preparation thereof and the use thereof in the manufacture of footware and related articles. It is known that thermoplastic polyurethanes having a hardness Shore A lower than 80 harden and solidify with difficulty. Therefore they are not suitable for being processed by extrusion, injection and moulding or have to remain in the moulds too long, thus making their processing cycle expensive. EP-A-0 134 455 teaches to reduce the hardness Shore A of a thermoplastic polyurethane having a hardness Shore A of from 95 to 80, and other specific features disclosed therein, by adding, to granules of the said polyurethane, from 11 to 100% (generally from 25 to 70%) by weight of a plasticizer selected among phthalic acid di(methoxyethylester), tricresyl phosphate and diphenyl cresyl phosphate. However, this prior art does not teach how to produce an elastic thermoplastic polyurethane which is rubber-like both at the sight and to the touch, wherein the hardness Shore A lower than 80 is a feature of the polymer per se which, furthermore, has properties such that it can be processed by extrusion, injection and moulding in fast processing cycles. It has now surprisingly been found that a thermoplastic polyurethane having both a hardness Shore A lower than 80 and the above properties can be produced according to claim 8. It is another object of this invention to provide a thermoplastic polyurethane having a hardness Shore A lower than 80 according to claim 1. The reaction is preferably carried out at a temperature of from 60 to 140°C and for a time of from 1 minute to 3 hours. Of course, the reaction time is substantially affected by the possible addition of a catalyst, as well as the type of catalyst used and amount thereof. As regards the type of catalyst, there are apparently no special requirements, and standard catalysts known in the chemistry of polyurethanes can be used. A typical example of a preferred catalyst is Dabco 33LV (TM) of Air Product. Additives of a known type may be added to the reaction mass to perform known functions without thereby departing from the teaching of this invention. Examples of possible additives are: pigments, mould release agents, plasticizers, stabilizers and the like. Examples of suitable plasticizers are: dioctyl phthalate and butyl benzyl phthalate. Preferably, their amount is lower than 15% and, more preferably, lower than 10% by weight. The reaction is carried out in a centrifuge. The working temperature is preferably of about 90°C and the time of from 5 to 15 minutes. The tangential speed of the centrifuge is preferably of from 10 to 100 m/sec. The polyurethane of this invention is prepared by reacting from 80 to about 120 parts by weight of the polyhydroxy compound whose OH number is 56 with from 22 to 33 parts by weight of MDI, 2.8-4.2 parts by weight of MEG, and optionally 2-15 parts by weight of a plasticizer such as butyl benzyl phthalate (Unimol TM , Bayer A.G.) together with a conventional catalyst and mould release agent. The elastic and non-sticky mass of this invention is rubber-like both at the sight and to the touch and has a hardness Shore A lower than 80. It is shredded according to conventional techniques. Thus a granulate is obtained which is suitable for being processed into manufactured articles by conventional techniques and machines for extruding, injecting, calendering and moulding of thermoplastic polymers. Said manufactured articles may be extracted from the moulds within a few minutes and are already sufficiently hard and elastic not to undergo permanent set during extraction from the moulds. The properties of the polyurethanes of this invention are so good that the injection cores can also be extracted from the moulds within from about 5 seconds to 5 minutes leaving the injection channels completely clear. Another feature of the polyurethane of this invention is that it can easily be glued with conventional adhesives commonly used in the footwear industry, such as TPU (thermoplastic polyurethane) two-component liquid polyurethane. The favourable properties (i.e. rubber-like both at the sight and to the touch, and high elastic flow) of the polyurethane of this invention make it particularly suitable for the production of those manufactured articles which undergo repeated stresses such as, for example, footwear and parts thereof and, in particular, for the production of soles for footwear. In this type of use another property thereof plays a particularly important role: its good adhesion to the glues used in the footwear industry. The typical features of a polyurethane of this invention will be better understood with reference to some typical compounds of the invention prepared according to Example 1. Polyurethane 1 Hardness Shore A 65 Density 1.2 g/cm 3 Ultimate elongation 400% Tensile strength 300 kg/cm 2 Tear resistance 160 kg/cm Abrasion resistance 40 mm 3 Acid and oil resistance good Hydrolysis resistance good Polyurethane 6 Hardness Shore A 65 Density 1.2 g/cm 3 Ultimate elongation 800% Tensile strength 320 kg/cm 2 Tear resistance 130 kg/cm Abrasion resistance 35 mm 3 Acids and oils good Hydrolysis resistance excellent The following examples have the aim of illustrating this invention without, however, limiting it in any way. Unless otherwise stated, in the following examples the term "parts" is used to mean parts by weight. EXAMPLE 1 4.07 parts of monoethylene glycol were reacted with the stoichiometric amounts of diisocyanate and polyhydroxy compound required to afford a polyurethane having a hardness Shore A of 65, at 90°C for 5-15 minutes in a centrifuge (tangential speed of from 10 to 100 m/sec). Note: hardness Shore A decreases as the amount by weight of the polyhydroxy compound increases. The following compounds were prepared: Polyurethane 1 diisocyanate MDI polyhydroxy compound adipic acid/monoethylene glycol polyester (molecular weight of from 1000 to 3000) Polyurethane 2 diisocyanate MDI polyhydroxy compound adipic acid/butanediol polyester (molecular weight of from 1000 to 3000) Polyurethane 3 diisocyanate MDI polyhydroxy compound polycaprolactone (molecular weight of from 1000 to 3000) Polyurethane 4 diisocyanate MDI polyhydroxy compound polyether obtained by polymerization of hydroxylated tetrahydrofuran compounds (molecular of from 1000 to 3000) EXAMPLE 2 The polymerized mass of Polyurethane 1 obtained according to Example 1 above was shredded and then injected into moulds suitable for forming samples having the features set forth in ASTM D412.C for tensile stress tests on rubber. On the samples obtained in this way elastic flow was measured at the following times; 5 minutes (1 minute in the machine and 4 minutes for placing the specimen onto the dynamometer), 1 day and 5 days. The samples were subjected to a tensile stress which caused them to elongate up to double (from 25 to 50 mm; tensile stress = 5 kg) and quadruple (from 25 to 100 mm; tensile stress = 6 kg) their original length. After one minute the specimen was released and its elastic flow measured. The results are shown in the following table. Time after moulding Length of the specimen (mm) after elongation Elastic flow after elongation twice 4 times twice 4 times 5 minutes 29 41 84% 78.6% 1 day 26 37 96% 84.0% 6 days 25.5 34 98% 88.0%

Claims: A thermoplastic polyurethane having a hardness Shore A lower than 80, characterized in that it is the product of reaction of: a) from 22 to 33 parts by weight of 4,4'-diphenylmethane-diisocynate (MDI), b) from 80 to 120 parts by weight of a polyhydroxy compound whose OH number is 56 selected among the adipic acid/butanediol, adipic acidlmonoethylene glycol (MEG) and adipic acid/hexanediol poliesters, polycaprolactones and polyethers obtained by polymerization of hydroxylated tetrahydrofuran compounds, and c) from 2.8 to 4.2 parts by weight of monoethylene glycol. A polyuretane according to claim 1, characterized in that the reaction mass further comprises a catalyst. A polyuretane according to any of claim 1 or 2, characterized in that the reaction mass further comprises conventional additives. A polyuretane according to claim 3, characterized in that the additive is a plasticizer. A polyuretane according to claim 4, characterized in that the plasticizer is dioctyl phthalate or butyl benzyl phthalate. A polyuretane according to claim 5, characterized in that dioctyl phthalate or butyl benzyl phthalate is present in an amount lower than 15% by weight. A polyuretane according to claim 5 or 6, characterized in that dioctyl phthalate or butyl benzyl phthalate is present in an amount lower than 10% by weight. A process for preparing a thermoplastic polyurethane having a hardness Shore A lower than 80, comprising reacting a) from 22 to 33 parts by weight of 4,4'-diphenylmethane-diisocynate (MDI), b) from 80 to 120 parts by weight of a polyhydroxy compound whose OH number is 56 selected among the adipic acid/butanediol, adipic acid/monoethylene glycol (MEG) and adipic acid/hexanediol polyesters, polycaprolactones and polyethers obtained by polymerization of hydroxylated tetrahydrofuran compounds, and c) from 2.8 to 4.2 parts by weight of monoethylene glycol characterized in that the reaction is carried out in a centrifuge. A process according to claim 8, characterized in that the reaction is carried out at a temperature of from 60 to 120°C and for a time of from 2 minutes to 3 hours. A process according to claims 8 and 9, characterized in that the reaction mass further comprises a catalyst. A process according to any of claims from 8 to 10, characterized in that the reaction mass further comprises conventional additives. A process according to claim 11, characterized in that the additive is a plasticizer. A process according to claim 12, characterized in that the plasticizer is dioctyl phthalate or butyl benzyl phthalate. A process according to claim 13, characterized in that dioctyl phthalate or butyl benzyl phthalate is present in an amount lower than 15% by weight. A process according to claims 13 or 14, characterized in that dioctyl phthalate or butyl benzyl phthalate is present in an amount lower than 10% by weight. A process according to claim 8, characterized in that the reaction is carried out at a temperature of about 90°C for a time of from 5 to 15 minutes. A process according to claim 8, characterized in that the centrifuge is driven at a tangential speed of from 10 to 100 m/sec. Use of a polyurethane according to any of claims from 1 to 7 for manufacturing footwears or parts thereof. Use of a polyurethane according to claim 18 for manufacturing soles for footwears. Footwears and parts thereof when manufactured with a polyurethane according to any of claims from 1 to 7. Soles for footwears which are manufactured with a polyurethane according to any of claims from 1 to 7. Use of a polyurethane prepared with a process according to any of claims from 8 to 17 for manufacturing footwears or parts thereof. Use of a polyurethane according to claim 22 for manufacturing soles for footwears. Footwears and parts thereof when manufactured with a polyurethane prepared with a process according to any of claims from 8 to 17. Soles for footwears which are manufactured with a polyurethane prepared with a process according to any of claims from 8 to 17.

Inventors: AUCI PIETRO, AUCI, PIETRO
Applicants: RUB THANE HOLDING S A, RUB-THANE HOLDING S.A.
Application year: 1994
Main classification: C08G18
IPC codes: C08G18, C08K5